人糠醛废水中回收醋酸

用活性炭预处理-电渗析浓缩醋酸-醋酸乙酯萃取新工艺,从糠醛废水中回收制备冰醋酸的中间试验取得了较好的结果。以电渗析法浓缩废水中醋酸,效率为80％。在脉冲筛板塔中,用醋酸乙酯萃取醋酸,萃取率达94％。精制得到冰醋酸(工业品二级标准),萃余液中醋酸乙酯回收,循环使用。     

废旧锌锰电池及其回收过程中汞载体的研究

针对目前一些回收废旧锌锰电池工艺在汞回收处理上存在的问题,集中对废旧锌锰电池中汞的载体以及回收处理废旧锌锰电池过程中汞载体的变化进行了研究,为废旧锌锰电池回收处理中汞的完全回收提供了依据.     

溶剂萃取法提取废旧碱性电池中的有价成分

为回收利用废旧电池，进行了溶剂萃取法提取碱性废弃电池中锌、锰金属的试验研究。选择南孚（AA）碱性废电池为处理样品，通过粉碎、水浸、酸浸等步骤，获得含锌、锰离子的稀溶液，并利用模拟体系得到的萃取结果进行浸出液的萃取性能试验研究。结果表明，每个废电池填充物中含锌和锰分别为0.25g和0.36g，具有可观的回收价值；采用完全皂化的二（2－乙基己基）磷酸（D2EHPA）／煤油为萃取剂提取含锌锰的酸浸出液，一级萃取就可获得60％以上的提取率。     

工业废水中盐酸,氯乙酸,醋酸共存时盐酸的测定

介绍了配水及工业废水中盐酸，氯乙酸，醋酸同时存在时，测定盐酸含量的方法。测定的相对标准偏为９．６９０％－０．９０３％，盐酸回收率为９３．４％－１０４．０％。     

从废旧锌锰电池中回收汞和铵的工艺研究

针对废旧锌锰电池中汞分散存在给回收处理废旧锌锰电池工作完全回收汞所带来的困难,利用汞和铵的性质特点,找到了从废旧锌锰电池中集中回收汞和铵的工艺条件,为废旧锌锰电池的资源化和防止二次污染创造了有利条件.     

衢州化工厂“三废”回收简讯

1.液碱槽车残液回收电化分厂液碱槽车内残留液碱与盐,以前是用自来水冲稀后直接排入下水。一九八○年九月烧碱车间建成回收装置。将槽车内残留的液碱与盐用水环真空泵抽入缓冲罐,经分离后,再用压缩空气压送至蒸发工段回收利用。投资9000元。去年回收30％液碱142吨,盐355吨。增加产值8.5万元,增加     

膜萃取和CaO-MgO乳状液反萃取法由醋酸废水生产醋酸钙镁盐

采用磺化聚醚砜中空纤维膜萃取醋酸废水,再用CaO—MgO乳状液反萃取制备醋酸钙镁盐。考察了膜萃取和反萃取的最佳实验条件。单级膜萃取醋酸废水（醋酸质量分数2％）的最佳条件为：水相走管程有机相走壳程（水外油内）逆流、有机相流量与水相流量比1．3、水相流量0．23mL/min,在此条件下萃取率可达74％;采用二级萃取,总萃取率可达95％。反萃取的最佳条件为：采用质量浓度100g／L的CaO—MgO乳状液作反萃取剂,CaO—MgO与醋酸摩尔比1．0：2．0,投料钙与镁摩尔比2．9：7．0,反萃取时间30min,室温,在此条件下反萃取率高于97％。     

利用药厂高锰酸钾还原残渣制二氧化锰

1.前言随着锰矿的日益枯竭及二氧化锰工业用量的增加,利用含锰废料回收锰,并制成各种锰盐,具有重要的经济和社会意义,这不但由废渣制得重要的化工原料,而且减少了含锰废渣对环境的污染。 2.探索性实验以东北制药总厂氯霉素车间高锰酸钾还原残渣(以下称MnO_2残渣)为原料,进行了制备二氧化锰的探索性实验。制备的工艺流程见下图。制备出的二氧化锰试剂的质量达到国家规定的三级标准。     

含稀醋酸废水中醋酸的回收方法

该发明涉及含稀醋酸废水中醋酸的回收方法,其特点是：先用电渗析法对含稀醋酸废水进行处理,获得质量浓度小于1000mg／L的醋酸极稀溶液,然后用阴离子交换树脂吸附法进一步脱除回收剩余的极稀溶液中的醋酸,使最后排除的废水中醋酸的质量浓度小于50mg／L。该方法将电渗析法与吸附法相结合,既克服了醋酸极稀溶液电导率低、电渗析过程电耗大的缺点,     

回收电解锰渣中的可溶性锰

以电解锰渣滤液为实验原料,研究了利用二氧化碳和氨水回收锰渣滤液中可溶性锰的工艺,实验结果表明:当n(氨水):n(可溶性锰)为2.50、二氧化碳曝气流量为50 L/h、曝气时间为5 min、振荡时间为60 min时,可溶性锰回收率达75%以上;对沉淀物进行X射线衍射分析,碳酸锰纯度接近100%。1kg电解锰渣可回收27 mg碳酸锰。     

回收萘法苯酐生产废水中的富马酸

采用催化异构化、碱溶、脱色、酸析、过滤等工艺处理萘法苯酐生产废水,回收其中的富马酸。考察了碱的品种、碱溶pH、活性炭加入量、酸析pH等对富马酸产品外观质量和收率的影响。实验得到最佳工艺条件:采用氢氧化钠作为碱溶用碱,碱溶pH为6,活性炭加入量为0.5%(w),酸析pH为2。在此最佳工艺条件下制备的富马酸产品外观为白色,纯度达到99.1%,产品收率为72.8%。按30 kt/a苯酐生产装置计,每年可回收富马酸660 t,年利润429万元。     

利用醋酸废水制取醋酸钙镁盐

用三辛胺萃取醋酸废水中的醋酸，加入白云石灰乳反萃、可制得环保型除冰剂醋酸钙镁盐（CMA）。研究了萃取剂组成，剂水比，萃取温度，萃取时间，搅拌速度对萃取效率的影响，确定了反萃的操作条件。试验表明：采用该法处理稀醋酸，工艺简单、醋酸利用率高。     

Tannic acid as a novel and green leaching reagent for cobalt and lithium recycling from spent lithium-ion batteries

Tannic acid–acetic acid is proposed as novel and green chemicals for cobalt and lithium recycling from spent lithium-ion batteries through a leaching process. The synergism of both acids was documented through batch and continuous studies. Tannic acid promotes cobalt dissolution by reducing insoluble Co³⁺ into soluble Co²⁺, while acetic acid is critical to improve the dissolution and stabilize the metals in the pregnant leach solution. Based on batch studies, the optimum conditions for metal recovery at room temperature are acetic acid 1 M, tannic acid 20 g/L, pulp density 20 g/L, and stirring speed 250 rpm (94% cobalt and 99% lithium recovery). The kinetic study shows that increasing temperature to 80 °C improves cobalt and lithium recovery from 65 to 90% (cobalt) and from 80 to 99% (lithium) within 4 h at sub-optimum condition (tannic acid 10 g/L). Kinetic modeling suggests the leaching process was endothermic, and high activation energy indicates a surface chemical process. For other metals, the pattern of manganese and nickel recovery trend follows the cobalt recovery trend. Copper recovery was negatively affected by tannic acid. Iron recovery was limited due to the weak acidic condition of pregnant leach solution, which is beneficial to improve leaching selectivity.

     

Hydrometallurgical recycling of cobalt from zinc plants residue

A large amount of hot filter cake (HFC) is annually generated in Iranian zinc plants. It contains 1% zinc, 16–30% manganese, 5–25% calcium and 1–4.5% cobalt. Usually, zinc is selectively leached by an alkaline medium and its residue is known as alkaline leached HFC (ALHFC). In the present study, the possibility of cobalt extraction from ALHFC was investigated using a creative hydrometallurgical process. At the first stage, zinc and cadmium were selectively removed with sulfuric acid. At the second stage, it was deeply focused on the possibility of selective reductive leaching of cobalt by H₂O₂ as a reductant in the presence of manganese. As results, several differences were found between the mechanism of cobalt and manganese leaching. Accordingly, cobalt leaching was more affected by acid concentration and manganese leaching was more affected by reductant concentration. Consequently, with manipulating these important parameters, it was made possible to selectively separate cobalt from manganese. Based on the obtained results, 90.9% of cobalt and only 10.04% of manganese were leached with 1% of H₂O₂. At the third stage, pregnant cobalt solution was successfully purified through a solvent extraction process with D2EHPA. Finally, cobalt hydroxide as our final product with a purity of more than 99% was precipitated from the pure pregnant solution at 70 °C.     

三维电极法处理含钴、锰废水

采用三维电极法对工业精对苯二甲酸(PTA)装置产生的含钴、锰废水进行处理.通过与传统二维电极法的处理效果进行比较,论证了三维电极法脱除Co2+,Mn2+的优越性.探究了填料类型、极板间电压、粒子电极填充比(粒子电极质量(g)与废水体积(mL)的比)、极板间距等工艺参数对Co2+,Mn2+脱除率的影响.实验结果表明,适宜...     

电渗析法处理低浓度乙酸废液的研究

用电渗析法处理配制的乙酸质量分类为２．５％左右的乙酸水溶液，浓缩液乙酸质量分数达到２０％，稀相出水乙酸质量分数至０．０２％；对影响处理过程的因素进行了探讨。     

薄膜负载型TiO_2光催化降解乙酸

利用TiCl_4水解法在玻璃表面制备纳米TiO_2光催化膜,考察了TiO_2光催化膜对乙酸光催化降解过程的影响因素.实验结果表明:使用活化温度为460℃、镀膜4次、表面积168 cm~2的TiO_2光催化膜处理500 mL0.667 mmoL/L的乙酸350 min时,乙酸降解率为80.0%,与等量TiO_2粉末相比光催化膜活性显著增加;当乙酸初始浓度c_0小于0.667 mmoL/L时,光催化降解过程可用Langmuir-Hinshelwood动力学方程来描述;TiO_2膜连续使用5次(30 h)时的光催化活性基本不变;用质量分数为5%的HCl溶液浸泡失去活性的光催化膜1 h,TiO_2光催化膜的活性可完全恢复.     

Recovery of nickel, cobalt and some salts from spent Ni-MH batteries

This work provides a method to help recover nickel, cobalt metals and some of their salts having market value from spent nickel-metal hydride batteries (SNiB). The methodology used benefits the solubility of the battery electrode materials in sulfuric or hydrochloric acids. The results obtained showed that sulfuric acid was slightly less powerful in leaching SNiB compared to HCl acid. Despite that, sulfuric acid was extremely applied on economic basis. The highest level of solubility attained 93.5% using 3N sulfuric acid at 90 degrees C for 3h. The addition of hydrogen peroxide to the reacting acid solution improved the level of solubility and enhanced the process in a shorter time. The maximum recovery of nickel and cobalt metals was 99.9% and 99.4%, respectively. Results were explained in the light of a model assuming that solubility was a first order reaction. It involved a multi-step sequence, the first step of which was the rate determining step of the overall solubility. Nickel salts such as hydroxide, chloride, hexamminenickel chloride, hexamminenickel nitrate, oxalate and nickel oleate were prepared. With cobalt, basic carbonate, chloride, nitrate, citrate, oleate and acetate salts were prepared from cobalt hydroxide Cost estimates showed that the prices of the end products were nearly 30% lower compared to the prices of the same chemicals prepared from primary resources.     

酸浸—萃取—沉淀法回收废锂离子电池中的钴

采用酸浸—萃取—沉淀法回收废锂离子电池中的钴。实验结果表明:废锂离子电池在600℃下煅烧5 h可将正极材料上的有机黏结剂与正极活性物质分离;正极活性物质在Na OH溶液浓度为2.0 mol/L、n(Na OH)∶n(铝)=2.5、碱浸温度为20℃的条件下碱浸反应1 h后,铝浸出率达99.7%;已除铝的正极活性物质在硫酸浓度为2.5 mol/L、H_2O_2质量浓度为7.25 g/L、液固比为10、酸浸温度为85℃的条件下酸浸反应120 min,钴浸出率高达98.0%;酸浸液在p H为3.5、萃取剂P507与Cyanex272体积比为1∶1的条件下,经2级萃取,钴萃取率为95.5%;采用H_2SO_4溶液反萃后在硫化钠质量浓度为8 g/L、反萃液p H为4的条件下沉淀反应10 min,钴沉淀率达99.9%。     

废聚苯乙烯硝化氧化制对硝基苯甲酸

研究了用聚苯乙烯废料为原料,经过硝化氧化制造具有高附加值的精细化工产品－对硝基苯甲酸。探讨了影响对硝基苯甲酸产率的因素,如硝酸的浓度和用量,压力,反应时间及催化剂用量等。结果表明,在优化条件下对硝基苯甲酸产率达５２％,产品纯度为９９％。